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  • B01J35/00—Catalysts, in general, characterised by their form or physical properties
  • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
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  • B01J35/613—10-100 m2/g
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  • B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
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  • B01J37/08—Heat treatment
  • B01J37/082—Decomposition and pyrolysis
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  • C01G25/006—Compounds containing zirconium, with or without oxygen or hydrogen, and containing two or more other elements
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  • B01J2523/30—Constitutive chemical elements of heterogeneous catalysts of Group III (IIIA or IIIB) of the Periodic Table
  • B01J2523/37—Lanthanides
  • B01J2523/3712—Cerium
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  • C01P2006/14—Pore volume

Definitions

• compositions having improved mercury intrusion volumes and surface areas and processes for making these compositions.
• the enhanced compositions disclosed herein contain zirconium, cerium, optionally yttrium, and optionally one or more rare earths other than cerium and yttrium.
• the processes for making these compositions utilize mesitylene within the process.
• Cerium and zirconium oxide (CeO 2 - ZrO 2 ) based materials have been used in catalytic applications. Introduction of zirconium into the cerium (IV) oxide lattice or cerium into the zirconium oxide lattice greatly enhances and facilitates oxygen mobility. This fact has been readily adapted by the automotive pollution control catalyst industry where cerium and zirconium oxide (CeO 2 - ZrO 2 ) containing materials are ubiquitous in use as washcoat components. These materials catalyze oxidation of carbon monoxide and hydrocarbons and reduction of nitrogen oxides as shown in the below equations:
• Cerium and zirconium oxide (CeO 2 - ZrO 2 ) based materials also have been used in catalytic applications as supports to disperse active metal catalysts so as to enhance the activity of the catalyst resulting in high turn-over numbers.
• the support plays a major role in maintaining the active metal catalyst's high dispersion state even at severe operating conditions such as high temperatures and hydrothermal environments.
• a support that fails to maintain its structural integrity under severe conditions may result in the occlusion or sintering of the active catalyst metal sites which results in diminished activity of the catalyst on a per molecule basis.
• cerium and zirconium based materials with excellent characteristics useful in catalysis and processes for providing these materials. That is, as a catalyst/catalyst support having a high surface area, a stable surface under oxidizing, reducing and hydrothermal and redox conditions, with stable crystallographic characteristics under severe aging conditions, high and stable mercury intrusion volume, with selective porosity /mercury intrusion volume, with high activity at lower temperatures and with low mass transfer resistance and high dynamic oxygen storage and release characteristics.
• the present compositions comprise zirconium, cerium, optionally yttrium, and optionally one or more rare earths other than cerium and yttrium.
• these compositions have a total mercury intrusion volume of from about 1.6 to about 4.0 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment. These compositions also can have a surface area of about 50 m 2 /g to about 100 m 2 /g after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment.
• the compositions further have a surface area of about 20 m 2 /g to about 85 m 2 /g after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment and in some embodiments, the compositions further have a total mercury intrusion volume of from about 1.0 to about 3.0 cc/g after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• these compositions have a total mercury intrusion volume of from about 2.0 to about 3.5 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment and a total mercury intrusion volume of from about 1.0 to about 2.0 cc/g after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• These compositions further can have a surface area of about 50 m 2 /g to about 70 m 2 /g after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment and about 20 m 2 /g to about 35 m 2 /g after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment.
• a process of producing a composition comprising zirconium, cerium, optionally yttrium, and optionally one or more rare earths other than cerium and yttrium.
• the process comprises the steps of: (a) mixing Zr and Ce salt solutions to provide a mixture; (b) adding the mixture to basic solution to form a precipitate; (c) dewatering the precipitate; (d) adding mesitylene to the precipitate; (e) supercritically drying the precipitate; and (f) calcining the precipitate to provide a composition comprising zirconium, cerium, optionally yttrium, and optionally one or more rare earths other than cerium and yttrium.
• the process further can include the step of washing the precipitate with water before dewatering the precipitate.
• the process also can include mixing rare earth solutions other than cerium and yttrium in step (a) and further mixing a yttrium solution in step (a) to provide the mixture.
• the compositions made by these processes have desirable mercury intrusion volumes and surfaces areas. Compositions made by this process are disclosed and as described above.
• the disclosed compositions can be used in catalysts for purifying exhaust gases or catalyst supports to improve heat resistance and catalyst activity when used with precious metal.
• These disclosed cerium and zirconium oxide (CeO 2 - ZrO 2 ) based materials possess high surface areas that have stable surfaces when subjected to severe aging conditions, such as under high temperature air, hydrothermal and redox conditions. They also possess stable crystallographic characteristics under severe aging conditions, high, stable, and selective mercury intrusion volumes, with high redox activities at lower temperatures and with low mass transfer resistance and high dynamic oxygen storage and release characteristics.
• FIG. 1 illustrates a flowchart of an embodiment of the experimental process of making high porosity cerium and zirconium with mesitylene added to the process as disclosed and described herein.
• FIG. 2A - 2C are graphs showing the difference in cumulative mercury intrusion volume of various cerium and zirconium compositions made by a prior art process in comparison to the process as disclosed herein using mesitylene after aging at 1000°C for 10 hours in an oxidizing environment and after aging at 1100°C for 10 hours in an oxidizing environment. Components listed in oxide equivalent ratios.
• FIGS. 2D - 2F are graphs showing the difference in aged surface areas of various cerium and zirconium compositions made by a prior art process in comparison to the process as disclosed herein using mesitylene after aging at 1000°C for 10 hours in an oxidizing environment and after aging at 1100°C for 10 hours in an oxidizing environment. Components listed in oxide equivalent ratios.
• FIGS. 3 A and 3B are graphs showing the typical increased mercury intrusion volume, of various cerium and zirconium compositions made by a prior art process in comparison to the process as disclosed herein using mesitylene for “as-produced” and after aging at 1000°C for 10 hours in an oxidizing environment and after aging at 1100°C for 10 hours in an oxidizing environment.
• reference to “a step” may include multiple steps, reference to “producing” or “products” of a reaction or treatment should not be taken to be all of the products of a reaction/treatment, and reference to “treating” may include reference to one or more of such treatment steps.
• the step of treating can include multiple or repeated treatment of similar materials/streams to produce identified treatment products.
• Numerical values with “about” include typical experimental variances.
• the term “about” means within a statistically meaningful range of a value, such as a stated particle size, concentration range, time frame, molecular weight, temperature, or pH. Such a range can be within an order of magnitude, typically within 10%, and even more typically within 5% of the indicated value or range. Sometimes, such a range can be within the experimental error typical of standard methods used for the measurement and/or determination of a given value or range. The allowable variation encompassed by the term “about” will depend upon the particular system under study, and can be readily appreciated by one of ordinary skill in the art.
• the present application relates to compositions having excellent mercury intrusion volumes and high surface areas after calcination. These compositions have advantageous properties for use as catalysts and/or catalyst components.
• the present application also relates to processes for preparing these compositions and compositions specifically prepared by the disclosed processes.
• mercury intrusion volume is determined using a Micromeritics Auto Pore IV mercury porosimeter using the following procedure: A powder sample was accurately weighed to 4 significant figures, and was then evacuated to 50 ⁇ m Hg in the machine sample holder. It was then subjected to mercury pressure (by the machine) with a filling pressure step of 0.5 psia. The dwell time at each step was 10 seconds. For the required conversion of pressure to pore entrance diameter, the value for mercury surface tension used was 485 dynes/cm and the contact angle used was 130°. The mercury intrusion volume was the integral of mercury intrusion volume into the sample at each pressure step.
• the mercury intrusion volume is associated with porosity and pore structure of catalyst/catalyst supports comprising cerium and zirconium. Regardless of the catalyst site activity, facile molecular transport of reactants to the active site and transport of reaction products away from the active site making it available for further reaction is of great importance. In situations where catalyst selectivity is of no consideration, a wide and open pore structure of the support is desirable. In situations where selectivity of the reacting molecules or products is desired, an engineered porosity allowing only the desired reactants to reach the active site and only the desired products allowed to leave the active site, is needed. For example, this type of function is well known and utilized with zeolitic materials. Therefore, materials with a particular mercury intrusion volume are beneficial depending on the types of desired reactions.
• the compositions comprise zirconium, cerium, optionally yttrium, and optionally one or more rare earths other than cerium and yttrium. These compositions have a total mercury intrusion volume of from about 1.6 to about 4.0 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment.
• the compositions have a total mercury intrusion volume of from about 1.8 to about 4.0 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment. In certain embodiments, these compositions have a total mercury intrusion volume of from about 2.0 to about 3.5 cc/g, and in other embodiments about 2.0 to about 3.0 cc/g, both after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment. In yet other embodiments, these compositions have a total mercury intrusion volume of from about 2.4 to about 2.6 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment.
• the compositions also can have a total mercury intrusion volume of about 1.0 to about 3.0 cc/g, after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• these compositions can have a total mercury intrusion volume of from about 1.0 to about 2.0 cc/g, and in some embodiments about 1.25 to about 2.0 cc/g, both after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• the compositions also can have a total mercury intrusion volume of about 1.3 to about 1.7 cc/g, after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• compositions further have a surface area of about 50 m 2 /g to about 100 m 2 /g after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment.
• these compositions can have a surface area of about 50 m 2 /g to about 70 m 2 /g, and in other embodiments 55 m 2 /g to about 65 m 2 /g, both after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment.
• the compositions also can have a surface area of about 20 m 2 /g to about 85 m 2 /g after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment. In some of these embodiments, the composition can have a surface area of about 20 m 2 /g to about 35 m 2 /g, and in other embodiments about 25 m 2 /g to about 30 m 2 /g, both after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment.
• the above-recited mercury intrusion volumes after calcination at 1000 and 1100 degrees Celsius for 10 hours in an oxidizing environment may be combined in any combination and further may be combined in any combination with the above-recited surface areas after calcination at 1000 and 1100 degrees Celsius for a period of 10 hours in an oxidizing environment.
• the above-recited surface areas after calcination at 1000 and 1100 degrees Celsius for 10 hours in an oxidizing environment may be combined in any combination and further may be combined in any combination with the above-recited mercury intrusion volumes after calcination at 1000 and 1100 degrees Celsius for a period of 10 hours in an oxidizing environment.
• the apparent surface area of the compositions was determined by using a Micromeritics ASAP 2000 system and nitrogen at about 77 Kelvin. The procedure outlined in ASTM International test method D 3663 - 03 (Reapproved 2008) was used but with one significant exception. It is well known that a "BET Surface Area” determination is not possible for materials that contain microporosity. Recognizing that the surface area is an approximation, the values reported are labeled "apparent surface area” values rather than "BET surface area” values. In compliance with commonly accepted procedures, the determination of apparent surface area, the application of the BET equation was limited to the pressure range where the term na(l - P/Po) of the equation continuously increases with P/Po. The out gassing of the sample was done under nitrogen at about 300 degrees Celsius for about 2 hours.
• the compositions also have a total mercury intrusion volume of from about 2.4 to about 2.6 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment.
• the compositions also have as a total mercury intrusion volume of from about 1.3 to about 1.7 cc/g after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• the compositions having any of the mercury intrusion volumes as set forth above also have a surface area of about 55 m 2 /g to about 62 m 2 /g after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment.
• compositions further have a surface area of about 25 m 2 /g to about 30 m 2 /g after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment.
• compositions as disclosed herein are made by the processes disclosed herein utilizing mesitylene. These compositions may have a total mercury intrusion volume of about 15% to about 80% greater, or about 15% to about 70% greater, after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment in comparison to compositions made by the same process but not utilizing mesitylene. These compositions may also have a total mercury intrusion volume of about 8% to about 45% greater, or about 8% to about 35% greater, after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment in comparison to compositions made by the same process but not utilizing mesitylene.
• the compositions made by the processes disclosed herein utilizing mesitylene have a surface area of about 5% to 45% greater, or about 5% to 25% greater, after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment in comparison to compositions made by the same process but not utilizing mesitylene.
• the compositions further may also have a surface area of about 5% to 30% greater, or about 5% to 25% greater, after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment in comparison to compositions made by the same process but not utilizing mesitylene.
• the molecular ratio of Zr/Ce is greater than 50%.
• the ratio of Zr to Ce (Zr:Ce) in the composition is about 1:1 to about 4:1, and in certain embodiments about 1:1 to about 2:1.
• any additional components e.g., yttrium, and rare earths other than cerium are present in an amount of 0 to 30% weight oxide based.
• the equivalent oxide weight ratio of CeO 2 /ZrO 2 /La 2 O 3 /Y 2 O 3 can be 45/45/5/5.
• the ratio of CeO 2 /ZrO 2 /La 2 O 3 /Nd 2 O 3 /Pr 6 O 11 can be 40/50/2/4/4.
• the ratio of CeO 2 /ZrO 2 /La 2 O3/Nd 2 O 3 can be 20.8/72.2/1.7/5.3.
• the ratio of CeO 2 /ZrO 2 /La 2 O 3 /Y 2 O 3 can be approximately 20-55 wt% / 35-75 wt% / 1-8 wt% / 1-8 wt%. In one example embodiment of these compositions, the ratio of CeO 2 /ZrO 2 /La 2 O 3 /Y 2 O 3 can be approximately 45 wt% / 45 wt% / 5 wt% / 5 wt%.
• the ratio of CeO 2 /ZrO 2 /La 2 O 3 /Nd 2 O 3 /Pr 6 O 11 can be 40 wt% / 50 wt% / 2 wt% / 4 wt% / 4 wt%. In other of these compositions, the ratio of CeO 2 /ZrO 2 /La 2 O 3 /Nd 2 O 3 can be 20.8 wt% / 72.2 wt% /1.7 wt% / 5.3 wt%. All compositions are referenced on an oxide equivalent basis.
• compositions as disclosed herein are made by a process comprising: (a) mixing Zr and Ce solutions to provide a mixture; (b) adding the mixture to a basic solution to form a precipitate; (c) dewatering the precipitate; (d) adding mesitylene to the precipitate; (e) supercritical drying the precipitate; and (f) calcining the precipitate to provide a composition comprising zirconium, cerium, optionally one or more rare earths other than cerium, and optionally yttrium,
• compositions made by this process exhibit a total mercury intrusion volume as described herein.
• these compositions have a total mercury intrusion volume of from about 1.6 to about 4.0 cc/g after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment.
• These compositions also can exhibit a surface area of about 50 m 2 /g to about 100 m 2 /g after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment.
• these compositions also exhibit a surface area of about 20 m 2 /g to about 85 m 2 /g after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment and a total mercury intrusion volume of from about 1.0 to about 3.0 cc/g after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• the compositions have a total mercury intrusion volume of from about 2.0 to about 3.5 cc/g, and in other embodiments about 2.0 to about 3.0 cc/g, both after calcination at 1000 degrees Celsius for 10 hours in an oxidizing environment.
• These compositions also may have a total mercury intrusion volume of from about 1.0 to about 2.0 cc/g, and in other embodiments about 1.25 to about 2.0 cc/g, both after calcination at 1100 degrees Celsius for 10 hours in an oxidizing environment.
• these compositions have a surface area of about 50 m 2 /g to about 70 m 2 /g, and in other embodiments 55 m 2 /g to about 65 m 2 /g, both after calcination at 1000 degrees Celsius for a period of 10 hours in an oxidizing environment.
• These compositions also may have a surface area of about 20 m 2 /g to about 35 m 2 /g, and in other embodiments about 25 m 2 /g to about 30 m 2 /g, both after calcination at 1100 degrees Celsius for a period of 10 hours in an oxidizing environment.
• the mesitylene can be added in an amount of approximately 50-100 % by weight with respect to oxide in the precipitate.
• the supercritical drying can be conducted at approximately 250 - 350°C and approximately 130-140 bars.
• the calcining can conducted at a temperature ranging from about 400°C to 1100°C and for from about 0.25 to 24 hours. In some embodiments, the calcining can be conducted at a temperature ranging from about 850°C to 1000°C and for about 3 to 7 hours, and in certain embodiments at a temperature of about 900°C and for about 5 hours. [0044] Calcining can be conducted in an oxidizing atmosphere, in an inert environment, or in a reducing atmosphere. If calcining is conducted in an inert or reducing environment, it may be followed by treatment in an oxidizing environment.
• the starting rare earth salts are water soluble and in the process as disclosed herein can be dissolved in water.
• the rare earth salts can be nitrates, chlorides, and the like.
• the cerium salt can be of Ce(III) or Ce(IV) oxidation state.
• the order of addition of the rare earths and the basic solution is not important and any order of addition may be utilized or all may be added together simultaneously. Further, the rate of addition is not important.
• the basic solution can be ammonia, sodium hydroxide, and the like.
• the precipitate may be washed to achieve a selected conductivity before calcining. In some embodiments this desired conductivity is about 6-8 mS/cm. In some embodiments, the precipitate is washed with water before the dewatering step.
• the dewatering step may be performed with any suitable alcohol, for example, isopropanol or ethanol.
• the precipitate is dewatered with ethanol.
• the calcining process provides the compositions as disclosed herein. Calcining can be conducted in any appropriate furnace and environment including, but not limited to, oxidizing, reducing, hydrothermal, or inert. In some embodiments, an oxidizing environment is preferred.
• a tubular furnace can be used.
• a tube furnace allows better gas flow for more thorough treatment.
• FIG. 1 is a flow chart for an embodiment of the process of making the compositions as disclosed herein.
• compositions as disclosed herein were made and tested for aged total mercury intrusion volume and specific surface areas and compared to similar compositions made according to a prior art process not using mesitylene.
• the compositions as disclosed herein and made by the processes disclosed herein exhibit improved cumulative mercury intrusion volume (Figs. 2A-2C) and improved specific surface area (SSA) (Figs. 2D-2F).
• compositions as disclosed herein exhibit an increased mercury intrusion volume in comparison to similar compositions made according to a prior art process not using mesitylene (See Figs 3A and 3B).
• a Ce/Zr/La/Nd/Pr nitrate precursor solution with appropriate cation ratios was prepared with the oxide equivalent content of 100g/L.
• the cerium used is of the ceric ammonium nitrate form.
• the mixed oxide materials comprising cerium and zirconium as described herein can be utilized as major components in a catalyst or catalyst support to be incorporated into automobile exhaust system.
• Introduction of zirconium into the cerium (IV) oxide lattice or cerium into the zirconium oxide lattice greatly enhances and facilitates oxygen mobility.
• doping these cerium and zirconium oxide (CeO 2 - ZrO 2 ) solid solution with other rare earths such as La, Nd, Pr and Y further improves catalytic activity and heat resistance.
• These mixed oxide materials as disclosed herein possess high surface areas that are thermally stable when subjected to severe aging conditions such as under high temperature air, hydrothermal and redox conditions. They also possess stable crystallographic characteristics under severe aging conditions, high and stable porosity with high and selective mercury intrusion volumes, with high redox activity at lower temperatures and with low mass transfer resistance and high dynamic oxygen storage and release characteristics.
• these cerium and zirconium mixed oxide powder is mixed with a refractory inorganic oxide, such as aluminium oxide, silicon oxide or titanium oxide, in water to form a powder slurry.
• a refractory inorganic oxide such as aluminium oxide, silicon oxide or titanium oxide
• precious metals such as palladium, rhodium or platinum
• other additives such as stabilizers, promoters and binders are added to the oxide slurry to obtain a washcoat.
• This washcoat slurry may then be coated onto a carrier, such as a ceramic monolithic honeycomb structure to prepare a catalyst for automobile exhaust gas purification.
• compositions and methods described herein are well adapted to attain the ends and advantages mentioned as well as those inherent therein.
• Those skilled in the art will recognize that the methods and systems within this specification may be implemented in many manners and as such are not to be limited by the foregoing exemplified embodiments and examples. In this regard, any number of the features of the different embodiments described herein may be combined into one single embodiment and alternate embodiments having fewer than or more than all of the features herein described are possible.

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• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Materials Engineering (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Physics & Mathematics (AREA)
• Thermal Sciences (AREA)
• Inorganic Chemistry (AREA)
• Catalysts (AREA)
• Exhaust Gas Treatment By Means Of Catalyst (AREA)
• Nanotechnology (AREA)

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• 2021
  • 2021-02-12 CN CN202180014223.1A patent/CN115461146B/zh active Active
  • 2021-02-12 WO PCT/IB2021/000099 patent/WO2021161108A1/en not_active Ceased
  • 2021-02-12 US US17/798,237 patent/US20230129838A1/en active Pending
  • 2021-02-12 CA CA3170188A patent/CA3170188A1/en active Pending
  • 2021-02-12 EP EP21715320.4A patent/EP3927461A1/de active Pending
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• 2022
  • 2022-08-05 ZA ZA2022/08817A patent/ZA202208817B/en unknown

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